✦ LIBER ✦

Dynamic hold-up in liquid metal irrigated packed beds

✍ Scribed by N. Standish

Publisher: Elsevier Science
Year: 1968
Tongue: English
Weight: 461 KB
Volume: 23
Category: Article
ISSN: 0009-2509
DOI: 10.1016/0009-2509(68)87034-4

No coin nor oath required. For personal study only.

📜 SIMILAR VOLUMES

Prediction of liquid phase hold-up in ra

Prediction of liquid phase hold-up in random packed beds

✍ D.M. Mohunta; G.S. Laddha 📂 Article 📅 1965 🏛 Elsevier Science 🌐 English ⚖ 308 KB

Experimental data on liquid phase hold-up in packed beds consisting of Raschig rings, Lessing rings and spheres are presented. A generalized correlation has been proposed for predicting the liquid phase hold-up in terms of packing density equivalent spherical diameter, liquid viscosity, density and

Hold-up in packed liquid-liquid extracti

Hold-up in packed liquid-liquid extraction columns

✍ T. Sitaramayya; G.S. Laddha 📂 Article 📅 1961 🏛 Elsevier Science 🌐 English ⚖ 380 KB

A generalized correlation for hold-up of dispersed phase in packed liquid extraction columns has been derived and used to correlate the data of the present investigation in 2 in. column along with the reported data in 3 in. to 12 in. columns for a wide variety of liquid systems using different sizes

Some observations on the static hold-up

Some observations on the static hold-up of aqueous solutions and liquid metals in packed beds

✍ N. Standish 📂 Article 📅 1968 🏛 Elsevier Science 🌐 English ⚖ 281 KB

Particle mass transfer and liquid hold-u

Particle mass transfer and liquid hold-up in packed beds with upward concurrent gas-liquid flow

✍ S. Mochizuki 📂 Article 📅 1981 🏛 Elsevier Science 🌐 English ⚖ 250 KB

Liquid flow non-idealities and hold-up i

Liquid flow non-idealities and hold-up in a pilot scale packed bed reactor with cocurrent gas-liquid upflow

✍ A.M. Thanos; P.A. Galtier; N.G. Papayannakos 📂 Article 📅 1996 🏛 Elsevier Science 🌐 English ⚖ 362 KB

Residence time distribution (R.T.D) experiments were carried out in a pilot scale upflow reactor. Feeds with properties similar to the properties of feeds at reaction conditions were used. The Piston-Dispersion model is used to decribe the liquid flow non-idealities. The effect of velocity and parti

Hold-up prediction in packed columns for

Hold-up prediction in packed columns for co-current gas—liquid downflow

✍ J.P. Reynier; J.C. Charpentier 📂 Article 📅 1971 🏛 Elsevier Science 🌐 English ⚖ 163 KB

Shorter Communications many authors, and the equation is identical to that derived by Lochiel and Calderbank [5]. For mass transfer to spherical drops or bubbles at high Reynolds number, the analysis of Moore [6] and Cheh and Tobias [7] can be applied to derive 2+3/~a/tLc l'45]t/~/.\_\_\_/bx.\_\_XlJ